| Couto et al. |
2013 |
type of fuel (wood), gasifier
type, operational conditions (temperature, pressure and oxidizing
agent). |
(13) |
| Richardson et al. |
2015 |
gasification reactors |
(15) |
| Molino
et al. |
2016 |
gasification reactors |
(8) |
| Singh et al. |
2016 |
feedstock type (cellulose,
hemicelluloses, and lignin), quality, and inherent moisture content,
particle size and density, operating conditions, steam (or other gasification
gas)-to-biomass ratio (S/B), air equivalence
ratio (ER), catalyst, SER (sorbent-to-biomass ratio) |
(9) |
| Sansaniwal et al. |
2017 |
pretreatment (drying, densification,
grinding), type of feedstock (cellulose, hemicelluloses, and lignin),
gasification reactors, operating parameters (temperature, pressure,
gasifying agents/media, ER, residence time) |
(10) |
| Thakkar
et al. |
2018 |
gasifier, operating parameters
(temperature, gasifying agents/media, ER, bed material, S/B, biomass
particle size, bed height) |
(11) |
| Gu et
al. |
2018 |
gasifying agent, gasification
temperature, ER |
(14) |
| Mishra et al. |
2021 |
hydrothermal technology,
gasifiers, gasification parameters (temperature, pressure, bed material,
type of biomass (cellulose, hemicelluloses and lignin), ER, residence
time, particle size, S/B |
(12) |
| |
|
feedstock type
(volatile,
ash, moisture), pretreatment (torrefaction, hydrothermal carbonation),
gasifiers, operating parameters (temperature, gasifying agents/media,
ER) |
|
